A method for continuously producing high-quality needle coke
A technology of needle coke and raw coke, applied in coking ovens, coking carbonaceous materials, petroleum industry, etc., can solve the problem that the coke pulling effect of the bulk mesophase cannot be achieved, the shear force is small, and the microstructure of needle coke cannot be realized uniaxial orientation, etc.
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Embodiment 1
[0024] The high-temperature coal tar is used as the feed material of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 18 hours, and the reaction temperature is 420°C. The pulse reaction process is regulated during the reaction residence time. That is, the reaction starts to control the high pressure of 1MPa for 3 hours, the pressure drops to 0.1MPa for 3 hours, then the pressure rises to 1MPa for 3 hours, then the pressure drops to 0.1MPa for 3 hours, and then the pulse reaction process is continuously carried out as a cycle. Continuous feed during the process until the end of the reaction cycle; after the reaction, the green coke is quickly transferred out of the carbonization reactor, the yield of green coke is 55.9%, the yield of liquid by-products is 35.3%, and the yield of gas by-products is 8.8% . The mesophase content of the obtained green coke is 1...
Embodiment 2
[0026] The low-temperature coal tar is used as the feed material of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 20 h, and the reaction temperature is 430 ° C. During the reaction residence time, the pulse reaction process is regulated. That is, the reaction starts to control high pressure 2MPa for 3 hours, the pressure drops to 1MPa for 3 hours, then the pressure rises to 2MPa for 3 hours, then the pressure drops to 1MPa for 3 hours, and then the pulse reaction process is continuously carried out as a cycle. Continuous feeding until the end of the reaction cycle; after the reaction, the green coke was quickly transferred out of the carbonization reactor, the yield of green coke was 58.7%, the yield of liquid by-products was 33.0%, and the yield of gas by-products was 8.3%. The mesophase content of the obtained green coke is 95%, and it is in the form o...
Embodiment 3
[0028]The vacuum residue is used as the feed of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 19h, and the reaction temperature is 435°C. The pulse reaction process is regulated during the reaction residence time , that is, the reaction starts to control the high pressure 2MPa for 2.5h, the pressure drops to 1.5MPa for 2.5h, then the pressure rises to 2MPa for 2.5h, then the pressure drops to 1.5MPa for 2.5h, and then continues to use this as a cycle Pulse reaction process, continuous feed during the reaction until the end of the reaction cycle; after the reaction, the green coke is quickly transferred out of the carbonization reactor, the yield of green coke is 60.5%, the yield of liquid by-products is 33.2%, and the yield of gas by-products The yield was 6.3%. The mesophase content of the obtained green coke is 100%, and it is in the shape of oriented...
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